EP1238770A2 - Catalyst for the low-temperature pyrolysis of hydrocarbon-containing polymer materials - Google Patents

Catalyst for the low-temperature pyrolysis of hydrocarbon-containing polymer materials Download PDF

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Publication number
EP1238770A2
EP1238770A2 EP99946572A EP99946572A EP1238770A2 EP 1238770 A2 EP1238770 A2 EP 1238770A2 EP 99946572 A EP99946572 A EP 99946572A EP 99946572 A EP99946572 A EP 99946572A EP 1238770 A2 EP1238770 A2 EP 1238770A2
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EP
European Patent Office
Prior art keywords
iron
metal
carbon
catalyst
pyrolysis
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP99946572A
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German (de)
English (en)
French (fr)
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EP1238770B1 (en
EP1238770A4 (en
Inventor
Oleg Volfovich Prilutsky
Emmanuil Volfovich Prilutsky
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Altimeco Ltd Oy
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Altimeco Ltd Oy
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Publication date
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Publication of EP1238770A4 publication Critical patent/EP1238770A4/en
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Publication of EP1238770B1 publication Critical patent/EP1238770B1/en
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Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • C10G1/10—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal from rubber or rubber waste
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
    • B01J21/18—Carbon
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/74—Iron group metals
    • B01J23/745—Iron
    • B01J35/40—
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/08—Heat treatment
    • B01J37/082—Decomposition and pyrolysis
    • B01J37/084—Decomposition of carbon-containing compounds into carbon
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/08—Heat treatment
    • B01J37/082—Decomposition and pyrolysis
    • B01J37/086—Decomposition of an organometallic compound, a metal complex or a metal salt of a carboxylic acid
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • C10G1/08—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal with moving catalysts
    • C10G1/086—Characterised by the catalyst used
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/04—Disintegrating plastics, e.g. by milling
    • B29B2017/0424—Specific disintegrating techniques; devices therefor
    • B29B2017/0496—Pyrolysing the materials
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2021/00—Use of unspecified rubbers as moulding material
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29L—INDEXING SCHEME ASSOCIATED WITH SUBCLASS B29C, RELATING TO PARTICULAR ARTICLES
    • B29L2030/00—Pneumatic or solid tyres or parts thereof
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00—Technologies for solid waste management
    • Y02W30/50—Reuse, recycling or recovery technologies
    • Y02W30/62—Plastics recycling; Rubber recycling

Definitions

  • the present invention relates to both the qualitative and quantitative composition of catalysts for the low-temperature pyrolysis of hydrocarbon-containing polymer materials, said catalysts being mainly intended for use in the recycling of waste rubber materials.
  • hydrocarbon-containing polymer materials refers preferably to composition materials capable of swelling in organic solvents, which contain the binders produced by either polymerization or copolymerization of alkenes, alkadienes, alkatriens, cycloalkenes, cycloalkadienes and cycloalkatriens and/or derivatives thereof, both alone and with a use of cross-linking agents, and usually not-readily-removable extenders, but preferably to compounded rubber based on vulcanized natural and/or synthetic rubber.
  • waste rubber materials refers to worn mechanical rubber articles irrespective of their design, initial sizes and designation.
  • waste rubber materials are the most routine form of hydrocarbon-containing polymer materials. Therefore, all that which will be said hereinafter about waste rubber materials might be attributed to other hydrocarbon-containing polymer materials capable of swelling in organic solvents. It as also evident for specialists that used tires of vehicles and, especially, metal-cord tires are presently the principal source of waste rubber materials. Therefore, all that which will be said hereinafter about waste rubber materials of used tires might be attributed to other waste rubber.
  • waste rubber materials can serve as a source of valuable recycled resources.
  • their recovery is impeded by high strength of chemical bonds in macromolecules of vulcanized rubber and by difficulties of rubber separation from reinforcing steel usually present in mechanical rubber articles.
  • most of the known methods and means for rubber destruction are dangerous because of the environmental contamination with sulfur compounds, carcinogenic carbon black and certain other toxic substances.
  • the processes include the trimming of tire beads, preliminary crushing of the trimmed tires into fragments, usually of about 3 cm in thickness, and:
  • the induction warming of metal cord eliminates the need for trimming beads; however, it increases an output of toxic rubber destruction products.
  • the electropulse destruction of cord wire (RU Patent 2050287) is based on discharging either a capacitor battery or an accumulation reactive LC-circuit on the metal cord. This process is characterized by a short-term heat emission with a high density of heat rating along boundaries of crystal grains of the metal and, consequently, by the bursting nature of cord wire destruction. At that, a considerable part of fine metal particles fly out of rubber tearing it to fragments of different sizes.
  • a critical index of their quality is activity that can be evaluated by their specific consumption per mass unit of the waste pyrolyzed, by minimal allowable temperature and pressure of the pyrolysis, by a degree of the polymer organic component conversion into low-molecular products, by a qualitative composition of such products, by their proportions in the mixture, and by their suitability for any subsequent use (with their minimal possible, or with no, additional processing prior to sale).
  • US Patent 3,996,022 discloses a catalyst for the pyrolysis in a form of a fusion of halides, for example zinc chloride and stannum chloride. At a temperature of above 300°C and a positive pressure, it ensures the transformation of waste rubber into a mixture of gaseous hydrocarbons, low-sulfur motor fuel and solid carbon residue.
  • a catalyst for the waste rubber pyrolysis is made of mica such as muscovite, sericite and biotite. It allows the process of pyrolysis of worn metal-cord tires to be led at a reaction temperature of 230 to 400°C under a pressure of 1.0-2.5 atmospheres.
  • Such a catalyst allows gaseous hydrocarbons, a wide range of liquid fuels, carbon black and a small amount of solid carbon residue, predominantly on cord wires, suitable for utilization as a metallurgical raw material to be produced in the absence of hydrogen, that is under significantly safer conditions.
  • a catalyst disclosed in UA Patent No. 10442 is the closest prior art for the proposed catalyst. It is produced as a product of the gaseous carbon oxide decomposition over iron scale and, in essence, represents a homogenous iron-carbon composition material in the form of ultra-dispersed iron particles and microscopic carbon particles.
  • This catalyst hereinafter referred to as "iron-carbon component” is added into hydrocarbon solvents of the used machine oil type in an amount of no less than 0.2%, and preferably from 0.5 to 1.0% of solvent's mass.
  • Waste rubber materials are left in this mixture till they swelled no less than 1.1 times, an excess of the solvent with the catalyst admixed is decanted for repeated use, while the waste rubber materials swelled are exposed to the pyrolysis at a temperature of 150 to 450°C, preferably near 200°C, in nitrogen current.
  • the entire condensate of liquid products of the pyrolysis produced with a use of the catalyst described constitutes, in essence, black oil fuel having a boiling onset temperature of over 150°C, a boiling end temperature of near 400°C and a flash temperature of over 100°C, which contains over 90% of paraffin-like hydrocarbons with the chain length of above C 5 .
  • the bound sulfur contents in the pyrolysis products not infrequently are below 1.0%.
  • the aim of the present invention is to provide, by means of the improvement in its content, a more active catalyst capable of facilitating both the condensate enrichment with light hydrocarbon fractions and the practically complete binding of sulfur in the pyrolysis products under processes of the pyrolysis of hydrocarbone-containing polymer materials.
  • a catalyst for the low-temperature pyrolysis of hydrocarbon-containing polymer materials which comprises an iron-carbon component in the form of microscopic carbon particles and ultra-dispersed iron particles, according to this invention, further comprises a metal-carbon component, which is obtained as a product of the stripping and the pyrolysis of a dispersion containing at least one salt of metals from the group VIII in the periodic table which is capable of decay upon heating in order to form an oxide, wherein said metal is selected from the group composed of iron, nickel and cobalt; as well as a carbohydrate and a highly volatile solvent.
  • the said complex catalyst as compared with the known catalyst in the form of single iron-carbon component, possesses higher activity in the processes of low-temperature pyrolysis of hydrocarbon-containing polymer materials and, particularly, waste rubber in the form of metal-cord tires, which is confirmed by:
  • the first supplemental difference consists in the fact that the iron-carbon component and the said metal-carbon component are taken in the following proportion (in percent by mass):
  • the second supplemental difference consists in the fact that said metal-carbon component is obtained as a product of the stripping and the pyrolysis of a dispersion, which, along with at least one salt of metals from the group VIII in the periodic table which is capable of decay upon heating in order to form an oxide, wherein said metal is selected from the group composing iron, nickel and cobalt, as well as a carbohydrate and a highly volatile solvent, contains an iron-carbon component which was obtained preliminary.
  • the resulting complex catalyst is characterized by the most uniform distribution of the iron- and metal-carbon components in mixture and thereby ensures a rise in the condensate output counting upon the organic part of rubber at the pyrolysis temperature of no more than 250°C.
  • the third supplemental difference consists in the fact that the metal-carbon component is a product of the stripping and the pyrolysis of a dispersion containing an iron salt, a carbohydrate and a highly volatile solvent. Iron is the most accessible metal among metals from the VIII group in the periodic table. Therefore, the catalyst according to this invention occurs to be most acceptable judging from both the production cost for manufacturers and the price for consumers.
  • the fourth supplemental difference consists in the fact that the metal-carbon component is a product of the stripping and the pyrolysis of a dispersion containing an iron salt, a carbohydrate selected from group consisting of mono- and disaccharides, and a highly volatile solvent. Mono- and disaccharides are accessible and pyrolyzed readily to ultra-dispersed carbon black, which allows the metal-carbon component of the proposed catalyst to be produced both cheaply and effectively.
  • the fifth supplemental difference consists in the fact that the metal-carbon component is a product of the stripping and the pyrolysis of a dispersion containing an iron salt, a water-soluble high-molecular carbohydrate selected from the group consisting of starch and water-soluble cellulose esters, and water as a highly volatile solvent.
  • the water dispersion containing such water-soluble polysaccharides proves to be most convenient to produce the metal-carbon component cheaply and with a high metal concentration.
  • the sixth supplemental difference consists in the fact that iron and carbon are present in the iron-carbon component in the following amounts (in mole-percent):
  • the seventh supplemental difference consists in the fact that iron and carbon are present in the metal-carbon component in the following amounts (in mole-percent):
  • the eighth supplemental difference consists in the fact that iron is present in the catalyst in the form of particles sized 50 to 8,000 ⁇ .
  • the catalyst of this invention represents a mixture of the iron- and metal-carbon components, which can be obtained as follows.
  • the iron-carbon component is to be produced first.
  • a weight of fine-dispersed ferric oxide or iron salt which can be decomposed by heat to form an oxide is taken in a crucible and heated up to a temperature of 500 to 600°C.
  • the ferric oxide is kept at this temperature in the current of a CO-containing gas with admixed hydrogen or hydrogen-containing components, such as water vapors.
  • iron/carbon ratio is controlled by the exposure duration within ranges of (in mole-percent) 1.35 - 46.15 for iron and 53.85 - 98.65 for carbon.
  • the longer exposure is, the less mole proportion of iron and the more mole proportion of carbon will be in the iron-carbon component that is obtained as a semiproduct or an intermediate product.
  • the CO decomposition ceases spontaneously because of the iron dispersing to ultra-dispersed particles whose surfaces are blocked completely by microscopic carbon particles, and reducing of the iron catalytic activity in Bell-Buduar reaction practically to zero.
  • iron particles are sized from some hundredth to some tenth parts of micrometer, while those of carbon from some tenth parts of micrometer to several tens of micrometers.
  • the iron-carbon component can contain such trace admixtures as ferric carbides and oxygen, with the latter being usually present in the form of secondary or unreacted iron oxides and, partly, in sorbate state.
  • the metal-carbon component can be produced independently of the iron-carbon component.
  • the dispersion is firstly prepared by the known method, i.e. by dosing and mixing, which, if necessary, can be carried out as the concurrent or successive triturating of solid ingredients in a liquid disperse medium, at that said dispersion being in the form of a solution or a suspension contains:
  • salts of the indicated type can be found preferably among formates and acetates as well as propionates and citrates of iron, cobalt and nickel.
  • formates and acetates as well as propionates and citrates of iron, cobalt and nickel.
  • other salts of mono-, di- and tricarboxylic acids is not excluded as well as nitrates and nitrites of said metals.
  • Carbonhydrate - reducers can be exemplified by:
  • Volatile solvents can be exemplified by the lower aliphatic alcohols used in preparing suspensions (sols), and preferably by distilled water, which is used usually in preparing true solutions or gels of reagents, selected for the production of the metal-carbon component under this invention.
  • the suspension prepared is concentrated by evaporation in an inert atmosphere until dry (possibly, under vacuum and/or at a higher temperature) and pyrolyzed in an inert atmosphere too with the stepped heating and an exposure at each stage, i.e.:
  • a "metal/carbon" ratio in the metal-carbon component is controlled by changing an amount of the metal source, that is of a selected salt(s), and an amount of the carbon source, that is of a selected carbohydrate (and, in a certain degree, a selected alcohol when alcohols are used as a disperse medium), in the dispersion prepared.
  • the metal-carbon component is mixed with the previously obtained iron-carbon component in a desired ratio.
  • Another, more preferable method for the new catalyst production provides for the preparation of a premixture by the introduction of the previously obtained iron-carbon component into a dispersion for preparing the metal-carbon component and the treatment, i.e. evaporation and pyrolysis, of this premixture, as above indicated.
  • This method ensures a substantial simplification of the mixture homogenization and a stabilized value of specific surface in various catalyst lots with the same ratio between the iron- and metal-carbon components.
  • the processes of pyrolysis run more stably, and the composition and quality of target products of the recycling waste rubber become stabilized.
  • the iron- and metal-carbon components were present in the mixture in the following amounts (in percent by mass):
  • iron in the finished catalyst according to this invention is present in the form of particles sized 50 to 8,000 ⁇ , and preferably 50 to 500 ⁇ .
  • the new catalyst reveals activity even at negative temperatures. Moreover, the studies on products of H 2 para-ortho-conversion with deuterium added have shown the presence of HD molecules, which indicates the breakage of bonds within H 2 molecules with the subsequent turning of the second atom into the orthoposition. Such an activity of the new catalyst is connected with the distinctive features of its structure, in which the metal-carbon "complexes" play a role of the active centers.
  • an average size of carbon particles amounts to some tenth parts of ⁇ m, that of metal particles some hundredth parts of ⁇ m, and specific surface of the powdery catalyst of about 100 m 2 /g and more, the amount of necessary catalytic additive comprises 0.2 to 0.5% by mass of the organic liquid used for swelling, in which the preliminary processing of waste rubber does take place.
  • the combination of swelling with catalytic action of the high-active powdery catalyst allows the pyrolysis to be carried out at temperatures of 250 to 400°C and the atmospheric pressure.
EP19990946572 1998-09-11 1999-08-25 Catalyst for the low-temperature pyrolysis of hydrocarbon-containing polymer materials Expired - Lifetime EP1238770B1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
UA98094786A UA45442C2 (uk) 1998-09-11 1998-09-11 Каталізатор низькотемпературного піролізу полімерних матеріалів, що містять вуглеводні
PCT/UA1999/000017 WO2000015403A2 (fr) 1998-09-11 1999-08-25 Catalyseur pour la pyrolyse a basse temperature de materiaux polymeres contenant des hydrocarbures

Publications (3)

Publication Number Publication Date
EP1238770A2 true EP1238770A2 (en) 2002-09-11
EP1238770A4 EP1238770A4 (en) 2006-12-13
EP1238770B1 EP1238770B1 (en) 2010-01-27

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EP19990946572 Expired - Lifetime EP1238770B1 (en) 1998-09-11 1999-08-25 Catalyst for the low-temperature pyrolysis of hydrocarbon-containing polymer materials

Country Status (16)

Country Link
US (1) US6743746B1 (zh)
EP (1) EP1238770B1 (zh)
JP (1) JP4680384B2 (zh)
KR (1) KR20020075769A (zh)
CN (1) CN1220550C (zh)
AT (1) ATE456644T1 (zh)
AU (1) AU776399B2 (zh)
CA (1) CA2383018C (zh)
DE (1) DE69941990D1 (zh)
DK (1) DK1238770T3 (zh)
ES (1) ES2340114T3 (zh)
PL (1) PL191172B1 (zh)
PT (1) PT1238770E (zh)
RU (1) RU2211086C2 (zh)
UA (1) UA45442C2 (zh)
WO (1) WO2000015403A2 (zh)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6743746B1 (en) * 1998-09-11 2004-06-01 Oy Altimeco Ltd Catalyst for the low-temperature pyrolysis of hydrocarbon-containing polymer materials
EP2085456A3 (en) * 2008-01-30 2009-12-16 Wilson, Paul Pyrolytic decomposition aparatus and use therefor and methof for pyrolytically decomposing organic substances
TWI795715B (zh) * 2020-08-14 2023-03-11 陳冠昕 觸媒、熱裂解裝置及熱裂解方法

Families Citing this family (22)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20080296205A1 (en) * 2005-12-06 2008-12-04 Yuji Kohara Waste Plastic Liquefaction Plant and Waste Plastic Liquefaction Process
EP2007744B1 (en) 2006-04-03 2017-05-17 Pharmatherm Chemicals Inc. Thermal extraction method for producing a taxane extract
EP1852490A1 (en) * 2006-05-05 2007-11-07 BIOeCON International Holding N.V. Pretreatment of particulate carbon-based energy carrier material
US7905990B2 (en) 2007-11-20 2011-03-15 Ensyn Renewables, Inc. Rapid thermal conversion of biomass
KR100967234B1 (ko) * 2008-04-11 2010-06-30 송소영 레저용 의자의 차양장치
WO2011034266A2 (en) * 2009-09-21 2011-03-24 Korea Research Institute Of Chemical Technology Apparatus for recovering styrene monomer and method of recovering styrene monomer using auxiliary solvent
US8519203B2 (en) * 2010-02-17 2013-08-27 Uop Llc Low oxygen biomass-derived pyrolysis oils and methods for producing the same
US20110284359A1 (en) 2010-05-20 2011-11-24 Uop Llc Processes for controlling afterburn in a reheater and for controlling loss of entrained solid particles in combustion product flue gas
US8499702B2 (en) 2010-07-15 2013-08-06 Ensyn Renewables, Inc. Char-handling processes in a pyrolysis system
US9441887B2 (en) 2011-02-22 2016-09-13 Ensyn Renewables, Inc. Heat removal and recovery in biomass pyrolysis
WO2012131485A1 (en) * 2011-03-31 2012-10-04 Percy Kean Technologies Pty. Ltd Process for separation of pure constituents
US9347005B2 (en) 2011-09-13 2016-05-24 Ensyn Renewables, Inc. Methods and apparatuses for rapid thermal processing of carbonaceous material
US10041667B2 (en) 2011-09-22 2018-08-07 Ensyn Renewables, Inc. Apparatuses for controlling heat for rapid thermal processing of carbonaceous material and methods for the same
US10400175B2 (en) 2011-09-22 2019-09-03 Ensyn Renewables, Inc. Apparatuses and methods for controlling heat for rapid thermal processing of carbonaceous material
US9044727B2 (en) 2011-09-22 2015-06-02 Ensyn Renewables, Inc. Apparatuses and methods for controlling heat for rapid thermal processing of carbonaceous material
US9109177B2 (en) 2011-12-12 2015-08-18 Ensyn Renewables, Inc. Systems and methods for renewable fuel
US9670413B2 (en) 2012-06-28 2017-06-06 Ensyn Renewables, Inc. Methods and apparatuses for thermally converting biomass
US10633606B2 (en) 2012-12-10 2020-04-28 Ensyn Renewables, Inc. Systems and methods for renewable fuel
US10337726B2 (en) 2015-08-21 2019-07-02 Ensyn Renewables, Inc. Liquid biomass heating system
CN106076335B (zh) * 2016-06-03 2019-04-26 浙江科技学院 一种非均相Fenton催化剂的制备方法和应用
CN110366448B (zh) 2016-12-29 2023-05-02 安辛可再生能源有限公司 液体生物质的脱金属化
WO2021204817A1 (en) 2020-04-07 2021-10-14 Total Research & Technology Feluy Purification of waste plastic based oil via a two steps hydrotreatment

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4656153A (en) * 1983-02-28 1987-04-07 Standard Oil Company (Indiana) Active carbon containing a dispersion of a metal component and method for making same
US5158983A (en) * 1991-10-04 1992-10-27 Iit Research Institute Conversion of automotive tire scrap to useful oils

Family Cites Families (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1607291A (en) 1925-10-02 1926-11-16 Marie Raymond Process for the recovery of the rubber and cotton contained in used motor-car pneumatic tires
US2447732A (en) 1945-07-16 1948-08-24 Campbell Rubber-reclaiming oil
US3996022A (en) 1974-05-17 1976-12-07 Tennessee Valley Authority Conversion of waste rubber to fuel and other useful products
JPS52125088A (en) 1976-04-12 1977-10-20 Toppan Printing Co Ltd Appartus for substituting gas
JPS5458704A (en) 1977-10-20 1979-05-11 Bridgestone Corp Hydrocracking of waste rubber
DE2900655A1 (de) 1979-01-10 1980-07-17 Phoenix Ag Verfahren zum trennen von gummi und metallbestandteilen aus gummibeschichteten stahlkordbestandteilen
JPS6014068B2 (ja) * 1983-03-25 1985-04-11 工業技術院長 プラスチツク廃棄物の熱分解法とその装置
US4740270A (en) 1986-06-19 1988-04-26 Universite Laval Vacuum pyrolysis of scrap tires
SU1698258A1 (ru) * 1988-07-07 1991-12-15 Институт высоких температур АН СССР Способ переработки отработанной шинной резины
DE3911082A1 (de) 1989-04-05 1990-10-18 Sen Alexander Faller Verfahren und vorrichtung zum wiederaufbereiten von gegenstaenden aus kunststoff und/oder gummi mit metallischen einlagen, insbesondere altreifen
EP0478774A4 (en) 1990-03-22 1992-09-09 Odessky Gosudarstvenny Universitet Method for extraction of metal reinforcement from rubber tyres
US5096570A (en) * 1990-06-01 1992-03-17 The United States Of America As Represented By The United States Department Of Energy Method for dispersing catalyst onto particulate material
AU636783B2 (en) * 1991-08-01 1993-05-06 Full Born Chen Industrial Co. Ltd. Process for producing oil and gas by cracking waste rubber
US5158982A (en) * 1991-10-04 1992-10-27 Iit Research Institute Conversion of municipal waste to useful oils
JPH06228568A (ja) * 1993-01-29 1994-08-16 Mazda Motor Corp 廃プラスチック又はゴム材から炭化水素油を得る方法及びその実施に使用される装置
US5286374A (en) * 1993-02-26 1994-02-15 Chen Huang Chuan Process for cracking waste rubber tires
US5385307A (en) 1993-12-27 1995-01-31 Azar; Essa T. Cryogenic tire recycling system
JP3430245B2 (ja) * 1994-05-18 2003-07-28 独立行政法人産業技術総合研究所 液状炭化水素及びカーボンブラックの製造方法
JPH0948980A (ja) * 1995-05-29 1997-02-18 Mitsui Petrochem Ind Ltd 合成重合体の分解による油状物の製造方法
CN1145395A (zh) * 1995-08-08 1997-03-19 周鼎力 利用废橡胶制造汽油、柴油和炭黑的方法及设备
UA28306A (uk) 1996-05-20 2000-10-16 Юрій Степанович Подзірей Пристрій для деструкції шин з металевим кордом
WO1999017874A1 (en) * 1997-10-08 1999-04-15 Corning Incorporated Method of making activated carbon-supported catalysts
UA45442C2 (uk) * 1998-09-11 2002-04-15 Емануїл Вольфович Прилуцький Каталізатор низькотемпературного піролізу полімерних матеріалів, що містять вуглеводні
CA2322733A1 (en) * 1999-10-14 2001-04-14 Toda Kogyo Corporation Porous composite particles and process for producing the same
US6686308B2 (en) * 2001-12-03 2004-02-03 3M Innovative Properties Company Supported nanoparticle catalyst

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4656153A (en) * 1983-02-28 1987-04-07 Standard Oil Company (Indiana) Active carbon containing a dispersion of a metal component and method for making same
US5158983A (en) * 1991-10-04 1992-10-27 Iit Research Institute Conversion of automotive tire scrap to useful oils

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See also references of WO0015403A2 *

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6743746B1 (en) * 1998-09-11 2004-06-01 Oy Altimeco Ltd Catalyst for the low-temperature pyrolysis of hydrocarbon-containing polymer materials
EP2085456A3 (en) * 2008-01-30 2009-12-16 Wilson, Paul Pyrolytic decomposition aparatus and use therefor and methof for pyrolytically decomposing organic substances
TWI795715B (zh) * 2020-08-14 2023-03-11 陳冠昕 觸媒、熱裂解裝置及熱裂解方法

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CN1220550C (zh) 2005-09-28
WO2000015403A3 (fr) 2000-05-25
JP4680384B2 (ja) 2011-05-11
CN1367813A (zh) 2002-09-04
US6743746B1 (en) 2004-06-01
CA2383018C (en) 2009-11-17
DK1238770T3 (da) 2010-05-10
DE69941990D1 (de) 2010-03-18
AU776399B2 (en) 2004-09-09
KR20020075769A (ko) 2002-10-05
ATE456644T1 (de) 2010-02-15
UA45442C2 (uk) 2002-04-15
AU5896299A (en) 2000-04-03
PT1238770E (pt) 2010-04-19
WO2000015403A2 (fr) 2000-03-23
PL191172B1 (pl) 2006-03-31
EP1238770B1 (en) 2010-01-27
EP1238770A4 (en) 2006-12-13
CA2383018A1 (en) 2000-03-23
RU2211086C2 (ru) 2003-08-27
ES2340114T3 (es) 2010-05-28
PL354201A1 (en) 2003-12-29

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